MX168697B - PROCEDURE FOR THE MANUFACTURE OF A CONDIMENT - Google Patents

PROCEDURE FOR THE MANUFACTURE OF A CONDIMENT

Info

Publication number
MX168697B
MX168697B MX004344A MX434486A MX168697B MX 168697 B MX168697 B MX 168697B MX 004344 A MX004344 A MX 004344A MX 434486 A MX434486 A MX 434486A MX 168697 B MX168697 B MX 168697B
Authority
MX
Mexico
Prior art keywords
hydrolyzate
head
column
insoluble
duct
Prior art date
Application number
MX004344A
Other languages
Spanish (es)
Inventor
Roland Faesi
Giancarlo Werner
Ursula Wolfensberger
Original Assignee
Nestle Sa
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Nestle Sa filed Critical Nestle Sa
Publication of MX168697B publication Critical patent/MX168697B/en

Links

Classifications

    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23L—FOODS, FOODSTUFFS OR NON-ALCOHOLIC BEVERAGES, NOT OTHERWISE PROVIDED FOR; PREPARATION OR TREATMENT THEREOF
    • A23L27/00—Spices; Flavouring agents or condiments; Artificial sweetening agents; Table salts; Dietetic salt substitutes; Preparation or treatment thereof
    • A23L27/10—Natural spices, flavouring agents or condiments; Extracts thereof
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23J—PROTEIN COMPOSITIONS FOR FOODSTUFFS; WORKING-UP PROTEINS FOR FOODSTUFFS; PHOSPHATIDE COMPOSITIONS FOR FOODSTUFFS
    • A23J3/00—Working-up of proteins for foodstuffs
    • A23J3/30—Working-up of proteins for foodstuffs by hydrolysis
    • A23J3/32—Working-up of proteins for foodstuffs by hydrolysis using chemical agents
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S203/00—Distillation: processes, separatory
    • Y10S203/19—Sidestream

Landscapes

  • Chemical & Material Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Polymers & Plastics (AREA)
  • Health & Medical Sciences (AREA)
  • Nutrition Science (AREA)
  • Engineering & Computer Science (AREA)
  • Food Science & Technology (AREA)
  • General Chemical & Material Sciences (AREA)
  • Biochemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
  • Seasonings (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

La presente invención se refiere a procedimiento de fabricación de un condimento, en el que se hidrolizan proteínas vegetales con ácido clorhídrico concentrado, se neutraliza el hidrolizado, se separan los primeros insolubles, se le deja reposar y se separan los segundos insolubles caracterizado por el hecho de que despues de la separación de dichos primeros o dichos segundos insolubles, se somete al hidrolizado a una destilación al vapor bajo presión reducida a la vez que se mantiene la densidad del hidrolizado a un valor sensiblemtne constante, de fin de eliminar el dicloro-1-3-propano-2-ol. Aparato de destilación comprendiendo una columan de destilación (1) compeusta de un cabezal (4), un cuerpo cilíndrico (2) provisto de elementos de contacto (3), y un fondo (5); un dispositivo de bombeo de gas (8, 9) conectado a dicho cabezal; un conducto de introducción (7) del hidrolizado conectado a dicha columna entre dicho cuerpo y el citado cabezal; un conducto de inyección (6) de vapor conectado a dicha columna entre el citado fondo y dicho cuerpo, y un conducto de evacuación (10) del hidrolizado, conectado a dicho fondo, caracterizado por el hecho de que además comprende un dispositivo de regulación (11) de la temperatura del hidrolizado conectado a dicho conducto de introducción (7) y por el hecho de que el diámetro del citado cabezal (4) es sensiblemente mayor que el diámetro de dicho cuerpo (2).The present invention refers to a seasoning manufacturing process, in which vegetable proteins are hydrolyzed with concentrated hydrochloric acid, the hydrolyzate is neutralized, the first insoluble ones are separated, they are left to stand and the second insoluble ones are separated, characterized by the fact that after the separation of said first or said insoluble seconds, the hydrolyzate is subjected to a steam distillation under reduced pressure while maintaining the density of the hydrolyzate at a constant constant value, in order to eliminate dichloro-1 -3-propane-2-ol. Distillation apparatus comprising a distillation column (1) complete with a head (4), a cylindrical body (2) provided with contact elements (3), and a bottom (5); a gas pumping device (8, 9) connected to said head; a conduit for introducing (7) the hydrolyzate connected to said column between said body and said head; a steam injection duct (6) connected to said column between said bottom and said body, and a hydrolyzate evacuation duct (10), connected to said bottom, characterized in that it also comprises a regulation device ( 11) of the temperature of the hydrolyzate connected to said introduction duct (7) and due to the fact that the diameter of said head (4) is appreciably greater than the diameter of said body (2).

MX004344A 1985-11-25 1986-11-13 PROCEDURE FOR THE MANUFACTURE OF A CONDIMENT MX168697B (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CH5013/85A CH668163A5 (en) 1985-11-25 1985-11-25 PROCESS FOR THE MANUFACTURE OF A CONDIMENT.

Publications (1)

Publication Number Publication Date
MX168697B true MX168697B (en) 1993-06-04

Family

ID=4286435

Family Applications (1)

Application Number Title Priority Date Filing Date
MX004344A MX168697B (en) 1985-11-25 1986-11-13 PROCEDURE FOR THE MANUFACTURE OF A CONDIMENT

Country Status (29)

Country Link
US (2) US4759944A (en)
EP (1) EP0226769B1 (en)
JP (1) JPH0614847B2 (en)
KR (1) KR910002663B1 (en)
CN (1) CN1019732B (en)
AR (1) AR240862A1 (en)
AT (1) ATE52892T1 (en)
AU (1) AU590352B2 (en)
BR (1) BR8605889A (en)
CA (1) CA1307972C (en)
CH (1) CH668163A5 (en)
DD (1) DD252535A5 (en)
DE (1) DE3671355D1 (en)
DK (1) DK163952C (en)
ES (1) ES2015249B3 (en)
FI (1) FI86684C (en)
GB (1) GB2183659B (en)
GR (1) GR3000629T3 (en)
IE (1) IE59094B1 (en)
IN (1) IN164293B (en)
MX (1) MX168697B (en)
MY (1) MY100339A (en)
NO (1) NO169042C (en)
NZ (1) NZ218386A (en)
OA (1) OA08489A (en)
PT (1) PT83802B (en)
RU (1) RU1773229C (en)
YU (2) YU43902B (en)
ZA (1) ZA868667B (en)

Families Citing this family (17)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0361595B1 (en) * 1988-09-26 1993-11-18 Unilever N.V. Process for preparing improved hydrolysed protein
DE68905561T2 (en) * 1988-09-26 1993-07-29 Unilever Nv METHOD FOR PRODUCING IMPROVED PROTEIN HYDROLYSATE.
EP0361596B1 (en) * 1988-09-26 1992-08-05 Unilever N.V. Process for preparing improved hydrolysed protein
US5102987A (en) * 1988-10-14 1992-04-07 Nestec S.A. Preparation of hydrolyzed protein having reduced α-chlorohydrin content
ATE75582T1 (en) * 1989-02-03 1992-05-15 Nestle Sa PROCESS FOR MAKING A SEASONING.
US4944953A (en) * 1989-05-19 1990-07-31 A. E. Staley Manufacturing Company Purification of hydrolysed protein with crystalline zeolite
CA2020461A1 (en) * 1989-07-14 1991-01-15 Donald J. Hamm Process for the production of hydrolyzed vegetable proteins and the product therefrom
IT1238663B (en) * 1989-10-24 1993-09-01 Panzani Ponte Liebig S P A PROCESS OF ACID HYDROLYSIS OF VEGETABLE PROTEINS FOR THE PRODUCTION OF PROTEIN EXTRACT WITH LOW CONTENT IN 3 MONOCHLOROPROPANDIOL AND WITH 1,2 DICHLOROPROPANOL IN A NON-DETECTABLE QUANTITY.
USH989H (en) 1990-07-13 1991-11-05 A. E. Staley Manufacturing Co. Purification of hydrolyzed protein by extraction
US5151503A (en) * 1991-03-28 1992-09-29 Nestec S.A. Process for reducing hydrolysed protein chlorohydrin content
CA2066378C (en) * 1991-04-24 2000-09-19 David J. Hardman Dehalogenation of organohalogen-containing compounds
US5532389A (en) * 1993-11-23 1996-07-02 The Dow Chemical Company Process for preparing alkylene oxides
US5972691A (en) * 1995-06-07 1999-10-26 Hercules Incorporated Dehalogenation of polyamine, neutral curing wet strength resins
FR2779447A1 (en) * 1998-06-04 1999-12-10 Angevine Biotech Production of plant protein hydrolysates with low content of chlorinated propanediols and propanols, useful as flavorings in human and animal foods
AU1525301A (en) * 1999-12-02 2001-06-12 Dsm N.V. Process for preparing improved protein hydrolysates
FR2817547B1 (en) * 2000-12-01 2003-08-22 Total Raffinage Distribution METHOD AND DEVICE FOR THE CONTINUOUS TREATMENT OF WASTE WATER OF INDUSTRIAL ORIGIN BY WATER VAPOR STRIPPING
JP7541406B1 (en) * 2023-09-14 2024-08-28 株式会社コスモテック Distillation Treatment Equipment

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US2251771A (en) * 1939-06-17 1941-08-05 Mid Continent Petroleum Corp Method of and apparatus for selecting fractions from fractionating condensers
US2364341A (en) * 1941-04-24 1944-12-05 Eastman Kodak Co Distillation control
DE1057437B (en) * 1953-08-20 1959-05-14 Tech Art Inc Machine for folding box blanks
US2873799A (en) * 1956-01-09 1959-02-17 Allied Chem Method and apparatus for dehydrating aqueous caustic solutions
DE1057435B (en) * 1956-11-12 1959-05-14 C H Knorr A G Process for removing excess hydrochloric acid during protein hydrolysis
US2991309A (en) * 1957-12-30 1961-07-04 Internat Minerals & Chemicals Protein hydrolysis
DE1159901B (en) * 1959-09-16 1963-12-27 Leybold Hochvakuum Anlagen Device for fractional distillation under vacuum
US3322650A (en) * 1964-01-03 1967-05-30 Phillips Petroleum Co Control of ratio of rate of heat flow to rate of feed in distillation responsive to bottoms analysis
US3503854A (en) * 1967-08-22 1970-03-31 Blaw Knox Co Dual stage steam stripping of vegetable oils at dual pressures
US3458404A (en) * 1967-12-11 1969-07-29 Shell Oil Co Apparatus for distilling liquids
US3542653A (en) * 1968-04-22 1970-11-24 Procter & Gamble Apparatus and process for continuous heat-bleaching and high temperature steam deodorization of edible oils
AU441069B2 (en) * 1968-04-24 1973-10-03 Blaw-Knox Company Process and apparatus for removing the remaining volatile substances from plant materials
US3692538A (en) * 1970-07-14 1972-09-19 Mayer & Co Inc O Method of preparing meaty-flavored protein hydrolyzates from meat carcass components
US3660247A (en) * 1970-07-31 1972-05-02 Du Pont Process and apparatus for controlling with a computer a distillation column product and heat fluid rates of flow
DE2212816C3 (en) * 1972-03-16 1974-12-12 Wiegand Karlsruhe Gmbh, 7505 Ettlingen Device for evenly distributing the liquid to be evaporated in a falling film evaporator
US3952109A (en) * 1973-02-13 1976-04-20 Far-Mar-Co., Inc. Low salt protein hydrolyzates
US4194017A (en) * 1975-08-26 1980-03-18 Societe D'assistance Technique Pour Produits Nestle S.A. Flavored bouillon base
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Also Published As

Publication number Publication date
AU590352B2 (en) 1989-11-02
DK562486A (en) 1987-05-26
EP0226769B1 (en) 1990-05-23
KR910002663B1 (en) 1991-05-03
NO864697D0 (en) 1986-11-24
DK562486D0 (en) 1986-11-24
IN164293B (en) 1989-02-11
FI86684B (en) 1992-06-30
NO169042B (en) 1992-01-27
JPH0614847B2 (en) 1994-03-02
MY100339A (en) 1990-08-28
CN86107674A (en) 1987-06-10
CA1307972C (en) 1992-09-29
KR870004665A (en) 1987-06-01
NZ218386A (en) 1989-04-26
OA08489A (en) 1988-07-29
GB2183659B (en) 1989-11-22
YU112587A (en) 1988-08-31
GR3000629T3 (en) 1991-09-27
NO169042C (en) 1992-05-06
YU47048B (en) 1994-12-28
EP0226769A1 (en) 1987-07-01
ZA868667B (en) 1987-06-24
AR240862A1 (en) 1991-03-27
CN1019732B (en) 1992-12-30
JPS62224256A (en) 1987-10-02
YU201486A (en) 1988-04-30
DD252535A5 (en) 1987-12-23
AR240862A2 (en) 1991-03-27
DK163952C (en) 1992-09-21
GB2183659A (en) 1987-06-10
CH668163A5 (en) 1988-12-15
PT83802B (en) 1989-05-12
FI86684C (en) 1992-10-12
DK163952B (en) 1992-04-27
DE3671355D1 (en) 1990-06-28
GB8627515D0 (en) 1986-12-17
YU43902B (en) 1989-12-31
IE862985L (en) 1987-05-25
ATE52892T1 (en) 1990-06-15
US4759944A (en) 1988-07-26
BR8605889A (en) 1987-08-25
ES2015249B3 (en) 1990-08-16
FI864489A0 (en) 1986-11-05
US4869785A (en) 1989-09-26
FI864489L (en) 1987-05-26
IE59094B1 (en) 1994-01-12
RU1773229C (en) 1992-10-30
AU6518186A (en) 1987-05-28
PT83802A (en) 1986-12-01

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